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A method for removing sodium from a hydrorefining agent carrier

A technology for hydrofining preparations and carriers, which is applied in catalyst carriers, chemical instruments and methods, catalyst activation/preparation, etc., can solve the problem of large amount of waste water discharge, reduce waste liquid discharge, ensure sodium removal efficiency, and shorten the removal of sodium. Effects of sodium time

Active Publication Date: 2018-06-26
CHINA NAT OFFSHORE OIL CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] The purpose of the present invention is exactly on the basis of above-mentioned prior art, provides a kind of method for desodiumization of hydrofinishing preparation carrier, this method solves the problem of The problem of desodiumization of hydrofinishing agent carrier and the large amount of wastewater discharge during the ammonium salt exchange process of hydrofinishing agent carrier

Method used

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  • A method for removing sodium from a hydrorefining agent carrier

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Effect test

Embodiment 1

[0036] Use ammonium sulfate 1 as the solute, at 2m 3 Prepare an aqueous ammonium salt solution with a mass fraction of 5% in the dissolution tank, and inject the prepared aqueous ammonium salt solution into three 1m 3 In the exchange tank (one-stage exchange tank 7, two-stage exchange tank 8, three-stage exchange tank 9), each exchange tank injects 600kg of ammonium salt solution. Control the temperature of each exchange tank at 55-65° C., add 120 kg of hydrofinishing agent carrier 4 into the hanging basket 3, add it into the primary exchange tank 7, and soak for 30 minutes. After the hanging basket is taken out from the primary exchange tank 7, 20 kg of the exchange liquid in the primary exchange tank 7 is discharged, and at the same time, the prepared fresh ammonium salt solution 6 is added to the primary exchange tank 7, and its mass ratio is higher than that of the discharged part. 2% more exchange fluid. Add the hydrogenation preparation carrier 4 in the hanging basket ...

Embodiment 2

[0039] Use ammonium carbonate as the solute, at 2m 3 Prepare an aqueous ammonium salt solution with a mass fraction of 5% in the dissolution tank, and inject the prepared aqueous ammonium salt solution into three 1m 3 In the exchange tank, each exchange tank is injected with 600kg of ammonium salt solution. Control the temperature of the exchange tank at 55-65°C, add 120kg of the hydrofinishing agent carrier into the hanging basket, add it to the primary exchange tank, and soak for 30 minutes. After taking out the hanging basket from the primary exchange tank, discharge 20kg of the exchange liquid in the primary exchange tank, and add the prepared fresh ammonium salt solution to the exchange tank at the same time, its mass is 2% more than the exchange liquid in the discharged part . Add the hydrogenated preparation carrier that has been exchanged and desodiumized once in the hanging basket to the secondary exchange tank and soak for 30 minutes. After the hanging basket is t...

Embodiment 3

[0042] Use ammonium acetate as the solute, at 2m 3 Prepare an aqueous ammonium salt solution with a mass fraction of 5% in the dissolution tank, and inject the prepared aqueous ammonium salt solution into three 1m 3 In the exchange tank, each exchange tank is injected with 600kg of ammonium salt solution. Control the temperature of the exchange tank at 55-65°C, add 120kg of the hydrofinishing agent carrier into the hanging basket, add it to the primary exchange tank, and soak for 30 minutes. After taking out the hanging basket from the primary exchange tank, discharge 20kg of the exchange liquid in the primary exchange tank, and add the prepared fresh ammonium salt solution to the exchange tank at the same time, its mass is 2% more than the exchange liquid in the discharged part . Add the hydrogenated preparation carrier that has been exchanged and desodiumized once in the hanging basket to the secondary exchange tank and soak for 30 minutes. After the hanging basket is tak...

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Abstract

The invention discloses a method for sodium removal of a hydrogenation refining agent carrier. The method adopts a three-stage exchange sodium removal way, and an ammonium salt exchanging liquid is recycled to carry out sodium removal. Sodium ions accumulated in the exchanging liquid are exhausted by discharging a little exchanging liquid, and part of fresh ammonium salt aqueous liquor is compensated during discharging, so that the ammonium ion mass concentration of the exchanging liquid in an exchange kettle is not lower than 1.0%, and the sodium ion mass concentration of the exchanging liquid is not greater than 0.05%. By using the method, in the premise of keeping the sodium removal effect and no damage of a pore structure of the hydrogenation refining agent carrier, the problem of large waste water discharge amount in the processes of hydrogenation refining agent carrier sodium removal and hydrogenation refining agent ammonium salt exchange is solved.

Description

technical field [0001] The invention relates to the technical field of chemical catalysis, in particular to a method for desodiumizing a hydrofinishing agent carrier. Background technique [0002] With the increasingly heavy and inferior crude oil in the world, at the same time, environmental protection regulations are increasingly light and clean diesel standards, especially the requirements for the content of sulfur and polycyclic aromatic hydrocarbons in diesel. In the future, the sulfur content in diesel will be lower than 10 μg / g, or even sulfur-free, and the content of polycyclic aromatic hydrocarbons will be lower than 1 wt%. The production of clean diesel oil with low sulfur, low aromatics and high cetane number has become an urgent task for the petroleum processing industry. The development of deep hydrodesulfurization and dearomatization technologies is of great significance. The key core technology lies in high activity and stable hydrogenation Development of Ref...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J37/30B01J32/00
CPCB01J37/30
Inventor 张玉婷于海斌张景成肖寒张国辉朱金剑张尚强宋国良彭雪峰王帅南军臧甲忠张雪梅
Owner CHINA NAT OFFSHORE OIL CORP